USPatentGranted
B1

Cleaning gas and method for cleaning vacuum treatment apparatus by flowing the cleaning gas

Granted 9 Dec 2003 · 6 office actions

Application
9480680
filed 11 Jan 2000
Publication
Not published
not published
Patent· this page
US 6,659,111
granted 9 Dec 2003

Life of the patent

11 dated events
⤢ drag to zoom20002002200420062008201020122014201620182020ProsecutionOwnershipTerm & fees
ProsecutionOwnershipTerm & feeshover for detail · click to open

Abstract

A cleaning gas includes HF gas whose concentration is greater than or equal to 1 vol % and oxygen containing gas whose concentration ranges from 0.5 to 99 vol %. The oxygen containing gas includes at least one of O2 gas, O3 gas, N2O gas, NO gas, CO gas and CO2 gas. The cleaning gas is employed to remove a deposited material generated in a vacuum treatment apparatus for producing a thin film of at least one of Ti, W, Ta, Ru, Ir, a compound thereof and an alloy thereof.

Description

9 parts
›BACKGROUND OF THE INVENTION

The present invention relates to a cleaning gas for removing an unnecessary deposit deposited on an inner wall and tools of a thin film producing apparatus by means of CVD method, and relates to a method for cleaning a vacuum treatment apparatus by the cleaning gas.

In various production processes for producing thin-film devices, optical devices and super steel materials, various films, powders and whiskers are produced by means of CVD method, sputtering method, sol-gel method and vapor deposition method. By the execution of the above-mentioned methods, unnecessary depositions are deposited on an inner wall and tools of the producing apparatus. In order to prevent such unnecessary deposit from affecting objective products, it is necessary to properly remove such unnecessary deposit. A cleaning gas employed to remove such unnecessary deposit is required to have several performances. For example, such a cleaning gas has to perform so as not to damage the objective products, not to increase the amount of particles in a reactor of the apparatus, to be easily varied into innocent gas and to tenderly affect the earth.

Presently, a plasma cleaning employing a cleaning gas of at least one of C 2 F 6 , CF 4 , C 4 F 8 , NF 3 and ClF 3 and a plasma-less cleaning employing a cleaning gas of at least one of F 2 , Cl 2 and ClF 3 have practically been executed to remove unnecessary deposits. However, these methods have several problems such that when the cleaning is executed by using the above-mentioned fluorine series gas, heat-resisting Ni-alloy, stainless steel and AlN are corroded by the gas and particles are increased in the apparatus, and that if the temperature for cleaning is lowered to suppress such corrosion, an idling time thereof is increased to lower the throughput of the apparatus, and that if the temperature for the cleaning is lowered to prevent the corrosion of the material of the apparatus, the cleaning speed is lowered.

A Japanese Patent Provisional Publication No. 8-295600 discloses a method for cleaning a nickel base plate employed to produce whiskers of TiC, TiCO and TiCN by means of diluted nitric acid. However, this method requires executing a wet cleaning in an in-site cleaning, and therefore it becomes difficult to improve the throughput of the apparatus.

›SUMMARY OF THE INVENTION

It is therefore an object of the present invention to provide an improved cleaning gas which effectively removes unnecessary deposit deposited in a vacuum treatment apparatus while satisfying performances required to such a cleaning gas.

A aspect of the present invention resides in a cleaning gas for removing a deposited material generated in a vacuum treatment apparatus for forming a thin film of at least one of Ti, W, Ta, Ru, Ir, a compound including one of Ti, W, Ta, Ru and Ir and an alloy including one of Ti, W, Ta, Ru and Ir, the cleaning gas comprises HF gas and oxygen containing gas.

Another aspect of the present invention resides in a method which functions to remove a deposited material generated in a vacuum treatment apparatus for forming a thin film of at least one of Ti, W, Ta, Ru and Ir, a compound including one of Ti, W., Ta, Ru and Ir and an alloy including one of Ti, W, Ta, Ru and Ir. The method comprises a step of flowing a cleaning gas in the vacuum treatment apparatus.

›BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a plan view showing a thin film producing apparatus of a cluster tool type, to which a cleaning method according to the present invention is adapted; and

FIG. 2 is a schematic view showing one of the thin film producing apparatus.

›DETAILED DESCRIPTION OF THE INVENTION · 1 of 2

As a result of intensive studies, the present inventors have found a composition of a cleaning gas by which unnecessary deposit deposited on an inner wall and tools of a film producing apparatus is efficiently and safety removed. More specifically, the cleaning gas according to the present invention functions to effectively remove unnecessary deposit deposited in a vacuum treatment apparatus for producing thin films of one of Ti, W, Ta, Ru and Ir, and of a compound of one of Ti, W, Ta, Ru and Ir, and alloy of one of Ti, W, Ta, Ru and Ir. The cleaning gas is a mixed gas containing a HF gas and an oxygen-containing gas. The concentration of the HF gas is greater than or equal to 1 vol %, and the concentration of the oxygen containing gas ranges from 0.5 to 99 vol %.

The oxygen containing gas employed in the cleaning gas according to the present invention comprises at least one of O 2 gas, O 3 gas, N 2 O gas, NO gas, CO gas and CO 2 gas.

The cleaning gas according to the present invention is applicable to the apparatus for making a thin film of one of Ti, W and Ta, a compound of one of Ti, W and Ta and an alloy of one of Ti, W and Ta. More specifically, Ti, W, Ta, an oxide of one of Ti, W and Ta, a nitride of one of Ti, W and Ta and an alloy of one of Ti, W and Ta. Furthermore, the cleaning gas is applicable to the apparatus for making a thin film of one of Ti, TiN, TiW, TiON, W, WN, TaN, Ru, Ir, compound thereof and alloy thereof. The cleaning gas simultaneously removes CVD reaction by-product produced at piping with by-product produced in the chamber of the apparatus.

It is preferable that the concentration of the HF gas of the cleaning gas is greater than or equal to 1 vol % and the concentration of the oxygen containing gas of the cleaning gas is within a range from 0.5 to 99 vol %. More preferably, the concentration of HF gas is greater than or equal to 10 vol % and the concentration of the oxygen containing gas is within a range from 1 to 90 vol %. If the concentration of HF gas is smaller than 1 vol % and the concentration of oxygen containing gas is smaller than 0.5 vol %, it is difficult to ensure a preferable etching speed. Specifically, when the concentration of oxygen containing gas is smaller than 0.5 vol %, the material of the apparatus is damaged by the cleaning gas in relatively large degree. Further, when the concentration of oxygen containing gas is greater than 1 vol %, an etching speed of the cleaning gas is accelerated. When the concentration of oxygen containing gas is greater than a range from 75 to 85 vol %, the etching speed tends to decrease in inverse proportion to the increase of the oxygen concentration. If the concentration of the oxygen containing gas is greater than 90 vol %, the etching speed is radically decreased.

In addition to the above-mentioned gases, inert gas such as N 2 , Ar, He may be employed. Further, the other gas having an oxidation property may be employed.

Next, as to the pressure during the cleaning operation employing the cleaning gas according to the present invention, it is necessary that the whole pressure, which is the sum of the HF gas partial pressure and the oxygen containing gas partial pressure, is smaller than or equal to 500 Torr. Preferably, the whole pressure should be smaller than or equal to 100 Torr, and it is further preferable that the pressure is within a range 0.1 to 10 Torr.

If the whole pressure becomes greater than 500 Torr, the evaluating time necessary for evacuating the cleaning gas becomes large. Further, even if a mixture ratio of the mixed gas is within an allowable range and if the partial pressure of the oxygen containing gas is smaller than or equal to 0.005 Torr, it is difficult to ensure a preferable etching speed, and the amount of particles in the reactor is increased without improving the corrosion resistance of the material of the apparatus.

As a result of further intensive studies, the inventors of the present invention have found that the corrosion resistance of the material employed in the apparatus. is remarkably improved by adding oxygen containing gas to HF gas. More specifically, the cleaning gas according to the present invention is applicable to (1) Al and Al-alloy such as A15052 and A16061 (JIS mark) at a temperature range not larger than 600° C., (2) heat-resisting Ni-alloy at a temperature range not larger than 450° C., (3) austenitic stainless steels at a temperature range of 450° C., (4) ferritic stainless steels at a temperature range of 460° C., (5) aluminum nitride at a temperature range not larger than 700° C., (6) aluminum oxide at a temperature range not larger than 920° C., (7) quartz at a temperature range not larger than 700° C., (8) silicon nitride at a temperature range of 760° C. and (9) silicon carbide at a temperature range of 680° C. That is, the cleaning temperature may be determined according to the employed material.

The present invention will be explained in detail with reference to the following examples. It will be understood that the present invention is not limited to these examples.

EXAMPLES 1 TO 14, COMPARATIVE EXAMPLES 1 AND 2

As to a sample produced by forming a Ti film of 1 μm thick on a silicon wafer, measurements of etching speed thereto under conditions shown in Table 1 were executed. The results thereof are also shown in Table 1. As is clearly shown in Table 1, the etching speed was remarkably improved by adding a trace quantity of O 2 gas. Also, when the O 2 gas had been changed to one of O 3 , N 2 O, NO, CO and CO 2 , the etching speed was similarly improved.

EXAMPLES 15 TO 22, COMPARATIVE EXAMPLES 3 AND 4

As to a sample produced by forming a TiN film of 1 μm thick on a silicon wafer, measurements of etching speed thereto under conditions shown in Table 2 were executed. The results thereof are also shown in Table 2. As is clearly shown in Table 2, the etching speed was remarkably improved by adding a trace quantity of O 2 gas. Also, when the O 2 gas had been changed to one of O 3 , N 2 O, NO, CO and CO 2 , the etching speed was similarly improved.

›DETAILED DESCRIPTION OF THE INVENTION · 2 of 2

EXAMPLES 23 TO 24, COMPARATIVE EXAMPLE 5

As to a sample produced by forming a W film of 1 μm thick on a silicon wafer, measurements of etching speed thereto under conditions shown in Table 3 were executed. The results thereof are also shown in Table 3. As is clearly shown in Table 3, the etching speed was remarkably improved by adding a trace quantity of O 2 gas. Also, when the O 2 gas had been changed to one of O 3 , N 2 O, NO, CO and CO 2 , the etching speed was similarly improved.

›Examples4
›EXAMPLE 25

As to a sample produced by forming a WN film of 1 μm thick on a silicon wafer, measurements of etching speed thereto under a condition that a temperature is 500° C., HF gas flow rate is 900 SCCM (90%), O 2 gas flow rate is 100 SCCM (10%). As a result, the lo etching speed was 3045 Å/min which is very high in etching speed. When O 2 gas had not been added, the etching speed was smaller than or equal to a measurement lower limit (≦1 Å/min).

It has not been confirmed of the damages of the apparatus due to the operations for examples 1 to 25.

EXAMPLES 26 TO 36, COMPARATIVE EXAMPLES 6 TO 16

As to Al, Al-alloy 5052 (JIS mark), Al-alloy 6061 (JIS mark), heat-resisting Ni-alloy (trade name: Hastelloy C-22), ferroalloy SUS316L (JIS mark), SUS304 (JIS mark), SUS430L (JIS mark), AlN, Al 2 O 3 , Si 3 N 4 , SiO 2 , corrosion characteristics by gas were observed. More specifically, HF gas (flow rate: 1000 SCCM) and a mixed gas of HF gas (flow rate: 100 SCCM) and N 2 O gas (flow rate: 10 SCCM) were used. The examples were exposed to the gas under a pressure of 500 Torr for 5 hours. After the exposure, the surface of each example was observed by an electron microscope, and the change of weights of each sample before and after the exposure was measured. As a result, it was found that damages to the material were remarkably decreased by adding N 2 O gas. Further, the etching speed of each of the examples 26 to 36 was very high as same as those of the examples 1 to 25. Comparative examples 6 to 16 show the results obtained by the experiments using only HF gas. Also when the gas N 2 O had been changed to one of O 2 , O 3 , NO, CO and CO 2 , the etching speed of this example was high as is similar to those of the examples 1 to 25.

COMPARATIVE EXAMPLE 17

The heat-resisting Ni-alloy (trade name: astelloy C-22) was exposed to the mixed gas of HF gas (flow rate: 1000 SCCM) and O 2 gas (flow rate: 1000 SCCM) at temperature 450° C. and under pressure 760 Torr for 5 hours As a result, the surface of the comparative example 17 was turned to yellow, and corrosive particles were generated.

›EXAMPLE 37

The heat-resisting Ni-alloy (trade name: Hastelloy C-22) was exposed to the mixed gas of HF gas (flow rate: 1000 SCCM) and O 2 gas (flow rate: 1000 SCCM) at a temperature of 450° C. and under a pressure of 500 Torr for 40 hours. As a result, a transparent passive film was formed on the surface of the example 37. The film was extremely thin and smooth. No corrosion was found on the surface.

COMPARATIVE EXAMPLE 18

The heat-resisting Ni-alloy (trade name: Hastelloy C-22) was exposed to the mixed gas of HF gas (flow rate: 990 SCCM) and O 2 gas (flow rate: 10 SCCM) at a temperature of 450° C. and under a pressure of 0.05 Torr for 40 hours. As a result, the surface of the comparative example 17 was turned to yellow and corroded. By an electron microscope, it was found that projecting substance and particulate material are generated on the surface of the comparative example 18. As a result of XMA observation, it was found that the particles produced on the surface of the comparative example 18 was a metal such as Fe and Ni and F.

COMPARATIVE EXAMPLE 19

An example obtained by forming TiW film of 1 μm thick on a silicon wafer was heated at 500° C., and HF gas (100%, flow rate: 1000 SCCM) was flowed in the reactor for 1 hour. Thereafter, the example was analyzed as to Ti and W by means of an X-ray fluorescence analyzer. As a result, Ti and W were remained on the wafer surface.

›EXAMPLE 38 · 1 of 2

An example obtained by forming TiW film of 1 μm thick on a silicon wafer was heated at 500° C., and the mixed gas of HF gas (flow rate: 1000 SCCM) and O 2 gas (flow rate: 1000 SCCM) was flowed in the reactor for 1 hour. Thereafter, the example was analyzed as to Ti and W by means of an X-ray fluorescence analyzer. As a result, Ti and W were not detected on the wafer surface.

EXAMPLES 39 to 52,

COMPARATIVE EXAMPLES 20 to 21

As to a sample produced by forming a Ta film of 1 μm thick on a silicon wafer, measurements of etching speed thereto under conditions shown in Table 5 were executed. The results thereof are also shown in Table 5. As is clearly shown in Table 5, the etching speed was remarkably improved by adding a trace quantity of O 2 gas. Also, when the O 2 gas had been changed to one of O 3 , N 2 O, NO, CO and CO 2 , the etching speed was similarly improved.

EXAMPLES 53 to 60, COMPARATIVE EXAMPLES 22 and 23

As to a sample produced by forming a TaN film of 1 μm thick on a silicon wafer, measurements of etching speed thereto under conditions shown in Table 6 were executed. The results thereof are also shown in Table 6. As is clearly shown in Table 6, the etching speed was remarkably improved by adding a trace quantity of O 2 gas. Also, when the O 2 gas had been changed to one of O 3 , N 2 O, NO, CO and CO 2 , the etching speed was similarly improved.

Next, a cleaning method for practically applying the above-mentioned gas to a vacuum treatment apparatus such as a thin film producing apparatus will be discussed.

FIGS. 1 and 2 show a thin film producing apparatus 2 of a cluster-tool type. The thin film producing apparatus 2 comprises a common conveying chamber 4 which has the form of octagon and is made of aluminum alloy. An articulated conveying arm 6 made of aluminum alloy is provided in the common conveying chamber 4 so as to be rotatable and expandable therein. A supporting portion for supporting a semiconductor wafer 50 to be treated is installed to a tip end of the articulated conveying arm 6 . Four thin-film producing apparatuses 8 A to 8 D are connected to the common conveying chamber 4 through gate valves G 1 to G 4 , respectively. A chamber 20 of each of the thin-film producing apparatuses 8 A to 8 D is made of aluminum alloy and includes a table 10 for setting the wafer 50 thereon, a clamp ring 28 for fixing the wafer 50 on the table 10 , a shower head 24 for flowing gas and an attachment ring therein. The table 10 is made of aluminum alloy. Spare chambers 12 A and 12 B are connected to the common conveying chamber 4 through gate valves G 5 and G 6 , respectively. The spare chambers 12 A and 12 B function as cooling chambers for cooling the treated wafer 50 . Cassette chambers 14 A and 14 B for storing a plurality of the wafers 50 are connected to the common conveying chamber 4 through gate valves G 7 and G 8 . It will be understood that a preheating chamber for preheating the wafer 50 before treatment may be provided as a spare chamber.

The thin-film producing apparatuses 8 A to 8 D, the common conveying chamber 4 , the spare chambers 12 A and 12 B, and the cassette chambers 14 A and 14 B are independently connected to a gas supply line 16 for supplying treatment gas, inert gas such as N 2 gas and the cleaning gas according to the present invention and to a gas evacuating line 18 for evacuating an inner ambient thereof.

In the thin-film producing apparatuses 8 A to 8 D, thin films of Ti, W, Ta, Ru, Ir, the compound thereof and the alloy thereof are produced by the thermal CVD method. Further, the plasma CVD method is executed by the provision of a high-frequency electric source for generating plasma, if necessary.

A representative thermal CVD method executed by using the thin-film producing apparatuses 8 A to 8 D will be discussed with reference to FIG. 2 .

The thin-film producing apparatus 8 A comprises the aluminum-alloy chamber 20 in which the table 10 providing a heater 22 therein is installed. The shower head portion 24 made of aluminum alloy is installed to a ceiling portion oppositely facing with the table 10 . A gas supply port 24 a of the shower head portion 24 is connected to the gas supply line 16 . A plurality of gas outlet ports 26 are provided at a bottom portion of the chamber 20 and are connected to the gas evacuating line 18 . The clamp ring 28 made of AlN (aluminum nitride) is provided around the table 10 so as to fix a wafer 50 on the table 10 . A ring-shaped attachment ring 30 is provided around the clamp ring 28 , as shown in FIG. 2 .

When a thin film of Ti or W is produced on the wafer 50 by using the above-mentioned thin-film producing apparatus 8 A, the thin film is also produced on the inner wall of the chamber 20 , exposed portions of the table 10 , the clamp ring 28 , the attachment ring 30 as an unnecessary film causing particles. The exposed portions of the table 10 are exposed to the cleaning gas. Therefore, it is necessary to execute a cleaning treatment for removing the unnecessary film attached on various portions at regular intervals or irregular intervals.

The examples 1 to 36 are employed in this cleaning method as a cleaning gas. If the examples 26 to 36 shown in Table 4 are employed as a cleaning gas, a mixed gas of HF gas (flow rate: 1000 SCCM) and N 2 O gas (flow rate: 10 SCCM) is used and the pressure is set at about 500 Torr. The cleaning temperature is set at about 500° C. within a range of 450 to 600° C.

In this condition, the etching speed of the cleaning gas with respect to TiN is about 4000 Å/min although this high speed is not shown in Table 4. This speed is generally the same as that in a case that the cleaning executed by means of ClF 3 gas at the temperature ranging from 200 to 300° C. Further, if ClF 3 gas is used at the high temperature 500° C., the table 10 , the shower head 24 , the clamp ring 28 and the attachment ring 30 will be corroded. In contrast, by using the cleaning gas according to the present invention, even at the temperature of 500° C., the corrosion of the various portions in the chamber 20 is prevented. That is, the film producing process is generally executed at the temperature ranging from 600 to 700° C., and the conventional cleaning process was generally executed at a temperature ranging from 200 to 300° C. In contrast, the cleaning process using the cleaning gas according to the present invention can be executed at the temperature ranging from 450 to 600° C. Therefore, the difference between the temperature in the film producing process and the temperature in the cleaning process is largely decreased by employing the cleaning gas according to the present invention. This enables the idling time for varying the temperature to be largely decreased. Consequently, this improves a throughput of the apparatus 2 . Further, it will be understood that cleaning an inner surface of the piping of the gas evacuating line is simultaneously executed with this cleaning of the chamber 20 .

›EXAMPLE 38 · 2 of 2

Herein, the cleaning gas may be diluted by mixing inert gas such as Ar, N 2 and He. Further, the cleaning may be executed at predetermined intervals. More specifically, it may be executed at each time when a predetermined number of the wafers were processed, or at each time when an accumulated time period for producing film reached a predetermined time period, or at regular intervals.

Furthermore, an after-treatment of the cleaning process may be executed by evacuating the cleaning gas from the chamber 20 and repeatedly supplying and stopping supplying inert gas such as N 2 gas to the chamber 20 , under a condition that the supply of the cleaning gas is stopped. If the repeated supply and stop of the inert gas are executed several times while evacuating gases from the chamber 20 , the cleaning gas will be rapidly discharged from the chamber 20 .

Additionally, the gas supply port 24 a of the shower head portion 24 may be divided into two ports which are connected to a cleaning gas supply line and a film-producing gas supply line, respectively. If such an arrangement of the plural supply ports 24 a is employed, inert gas such as N 2 gas is flowed in the film-producing gas supply line during the cleaning process. This prevents the cleaning gas from inversely flowing to and remaining in the film-producing gas supply line. Accordingly, the affect of the remaining cleaning gas to the next film producing process is prevented.

Furthermore, although the explanation of the cleaning process is discussed as to the film producing apparatus 8 A, it will be understood that the other film producing apparatuses 8 B to 8 D may execute the normal film forming process during the cleaning process of the film producing apparatus 8 A or may independently execute the cleaning process.

Although the embodiment of the cleaning method has been shown and described such that only the film producing apparatus 8 A executes the cleaning process, it will be understood that several or all of the film producing apparatuses 8 A to 8 D may simultaneously execute the cleaning process together with the common conveying chamber 4 . In this case, the pressures of the respective chambers are equalized at the same pressure by supplying inert gas before the cleaning. Thereafter, the corresponding gate valves are opened, and the cleaning gas is supplied to the respective gas supply line 16 . Furthermore, simultaneously with this supply, the evacuation through the respective gas evacuating lines 18 is executed. This enables the several chambers to be simultaneously cleaned by the cleaning process.

Furthermore, in such a situation, the spare chambers 12 A and 12 B and the cassette chambers 14 A and 14 B may be simultaneously cleaned by this cleaning process.

Although the cleaning gas and method according to the present invention has been shown and described such that the cleaning gas is independently supplied to the film producing apparatus, the common conveying chamber, the spare chamber and the cassette chamber, it will be understood that the present invention is not limited to this embodied method and may be supplied to each of several blocks constituted by several chambers. This enables the number of the gas supply lines to be decreased. Furthermore, if it is arranged such that all of the chambers are simultaneously executed, it is possible to decrease the number of the gas supply lines to one.

Although the embodied cleaning gas and method according to the present invention has been mainly shown and described as to the removal of the thin film of Ti, W, compound thereof and alloy thereof, it will be understood that the invention is not limited to these and may be applicable to the removal of the thin film of Ta, Ru, Ir, the compound thereof and the alloy thereof.

Further, although the embodied cleaning gas and method according to the present invention has been shown and described to employ the CVD method, the invention is not limited to this and may be applied to a vacuum treatment apparatus which generates the above mentioned compound and alloy in a treatment chamber due to a main treatment. Furthermore, although the embodied cleaning method according to the present invention has been shown and described as to the apparatus for treating a semiconductor wafer, the invention is not limited to this and may be applied to an apparatus treating a LCD substrate or glass substrate.

With the cleaning gas and the cleaning method of a vacuum treatment apparatus in accordance with the present invention, it becomes possible to ensure superior advantages. More specifically, by employing the cleaning gas according to the present invention to clean the vacuum treatment apparatus, it becomes possible to remove an unnecessary film deposited in the vacuum treatment apparatus, which produces a thin film of Ti, W, Ta, Ru, Ir, the compound thereof and the alloy thereof, at a relatively high temperature near the film producing temperature and at high etching speed and to prevent the apparatus from being damaged by corrosion. Therefore, it is possible to decrease a difference between the temperatures in film producing process and in cleaning process. This enables the idling time for varying the temperature to be decreased. Consequently, it is possible to remarkably improve an yield factor of products and a throughput of the producing apparatus employing the cleaning gas and the method using the gas according to the present invention.

The entire disclosure of Japanese Patent Application No. 11-302715 filed on Nov. 24, 1999 including specification, claims, drawings and summary are incorporated herein by reference in its entirety.

›Tables in the description — 6
TABLE 1
Tempera-Gas flowGas con-Etching
tureamountcentrationPressurespeed
(° C.)(SCCM)(vol %)(Torr)(Å/min)
Comparative500HF:1000HF:1005103
Example 1
Example 1500HF:1000HF:99.55298
O2:5O2:0.5
Example 2500HF:1000HF:9951660
O2:10O2:1
Example 3500HF:1000HF:90.958710
O2:100O2:9.1
Example 4500HF:300HF:85.752490
O2:50O2:14.3
Example 5500HF:1000HF:50510340
O2:1000O2:50
Example 6500HF:1000HF:40510305
O2:1500O2:60
Example 7500HF:1000HF:33.3510426
O2:2000O2:66.7
Example 8500HF:1000HF:25510319
O2:3000O2:75
Example 9500HF:1000HF:20510229
O2:4000O2:80
Example 10500HF:1000HF:12.559875
O2:7000O2:87.5
Example 11500HF:500HF:1058136
O2:4500O2:90
Example 12500HF:10HF:15238
O2:990O2:99
Comparative500HF:5HF:0.5599.4
Example 2O2:995O2:99;5
Example 13600HF:1000HF:90.9511900
O2:100O2:9.1
Example 14700HF:1000HF:90.9513810
O2:100O2:9.1
TABLE 2
Tempera-Gas flowGas con-Etching
tureamountcentrationPressurespeed
(° C.)(SCCM)(vol %)(Torr)(Å/min)
Comparative500HF:1000HF:10058.5
Example 3
Example 15500HF:1000HF:99.55926
O2:5O2:0.5
Example 16500HF:1000HF:9951400
O2:10O2:1
Example 17500HF:1000HF:90.951760
O2:100O2:9.1
Example 18500HF:1000HF:5052500
O2:1000O2:50
Example 19500HF:500HF:1051120
O2:4500O2:90
Example 20500HF:10HF:15238
O2:990O2:99
Comparative500HF:5HF:0.55140
Example 4O2:995O2:99.5
Example 21600HF:1000HF:90.954300
O2:100O2:9.1
Example 22700HF:1000HF:90.958200
O2:100O2:9.1
TABLE 3
Tempera-Gas flowGas con-Etching
tureamountcentrationPressurespeed
(° C.)(SCCM)(vol %)(Torr)(Å/min)
Comparative500HF:1000HF:1005≦1
Example 5
Example 23500HF:1000HF:9951800
O2:10O2:1
Example 24500HF:1000HF:90.952870
O2:10O2:9.1
TABLE 4
MaterialTemperature
(JIS mark)(° C.)Observation result
ComparativeAl400White thick film was deposited
Example 6and the film was cracked
ComparativeAl5052400(Comparative example 6 to 8)
Example 7
ComparativeAl6061400
Example 8
ComparativeHeat-400Surface of each comparative
resistingexamples 9 to 12 was
Example 9Ni alloyturned to yellow or black and
ComparativeSUS316400was cracked.
Example 10
ComparativeSUS3O4400
Example 11
ComparativeSUS430450
Example 12
ComparativeAlN700Corrosive particulates were
Example 13generated on the surface of each
ComparativeAl2O3900comparative examples 13-14.
Example 14
ComparativeSiO2700The surface of each comparative
Example 15example was etched to lose
ComparativeSi3N4700transparency, and the weight
Example 16thereof was decreased by the
etching.
Example 26Al600Semitransparent film was
Example 27Al5052600produced on the surface of each
Example 28Al6061600comparative example 26-32 and
Example 29Heat-450was in a passive state.
resistingTherefore, no corrosion
Ni alloywas occurred.
Example 30SUS316450
Example 31SUS304450
Example 32SU5430460
Example 33AlN700The weight and surface
Example 34Al2O3900condition of each example 33
Example 35SiO2700to 35 were not substantially
changed as corrpared with those
of each example before
treatment.
Example 36Si3N4760A semitransparent film was
formed on the surface of the
example 36. The surface was
smooth and had no corrosion.
Si-O bonding was observed as a
result of the analysis of ESCA.
It is thought that an oxide film
superior in corrosion was formed
on the surface.
TABLE 5
Tempera-Gas flowGas con-Etching
tureamountcentrationPressurespeed
(° C.)(SCCM)(vol %)(Torr)(Å/min)
Comparative500HF:1000HF:100529
Example 21
Example 39500HF:1000HF:99.55128
O2:5O2:0.5
Example 40500HF:1000HF:995460
O2:10O2:1
Example 41500HF:1000HF:90.95960
O2:100O2:9.1
Example 42500HF:300HF:85.751340
O2:50O2:14.3
Example 43500HF:1000HF:5056960
O2:1000O2:50
Example 44500HF:1000HF:4057342
O2:1500O2:60
Example 45500HF:1000HF:33.357132
O2:2000O2:66.7
Example 46500HF:1000HF:2557369
O2:3000O2:75
Example 47500HF:1000HF:2057089
O2:4000O2:80
Example 48500HF:1000HF:12.554958
O2:7000O2:87.5
Example 49500HF:500HF:1052685
O2:4500O2:90
Example 50500HF:10HF:15265
O2:990O2:99
Comparative500HF:5HF:0.5532.2
Example 22O2:995O2:99.5
Example 51600HF:1000HF:90.958872
O2:100O2:9.1
Example 52700HF:1000HF:90.959810
O2:100O2:9.1
TABLE 6
Tempera-Gas flowGas con-Etching
tureamountcentrationPressurespeed
(° C.)(SCCM)(vol %)(Torr)(Å/min)
Comparative500HF:1000HF:10050.5
Example 23
Example 53500HF:1000HF:99.5554
O2:5O2:0.5
Example 54500HF:1000HF:995258
O2:10O2:1
Example 55500HF:1000HF:90.951692
O2:100O2:9.1
Example 56500HF:1000HF:5051870
O2:1000O2:50
Example 57500HF:500HF:105380
O2:4500O2:90
Example 58500HF:10HF:1593
O2:990O2:99
Comparative500HF:5HF:0.5528
Example 24O2:995O2:99.5
Example 59600HF:1000HF:90.952396
Q2:100O2:9.1
Example 60700HF:1000HF:90.953986
O2:100O2:9.1

Claims

11 · 1 independent · depth 2
1234567891011
11 granted claims

Classifications

13 codes
IPC · International Patent Classification
Section C — Chemistry; metallurgy
  • C23F1/12
  • C23C16/44
Section H — Electricity
  • H10P14/24
  • H10P14/60
USPC · US Patent Classification
134/22.1134/22.18134/30134/31134/25.1134/26134/11134/2438/905

Claim changes

Soon
Coming soonHow the claims changed between publication and grant

See which claims were amended, added or cancelled during examination, with every added and removed word marked.

AmendedAddedCancelledUnchanged

The published claims of this patent are not paired with the granted ones in what we hold.

File wrapper

⤢ drag to zoomJan 2000Jul 2000Jan 2001Jul 2001Jan 2002Jul 2002Jan 2003Jul 2003Jan 2004USPTOApplicantNon-final rejectionResponse after non-finalRequest for continued examinationResponse after non-final
USPTOApplicanthover for detail · click to open
Pendency
3.9 y
1,428 days filing → grant
Office actions
3
non-final + final
Responses
2
1 RCE
Examiner
Randy Gulakowski
art unit 1746 · TC 1700
Citations: 14 back · 299 forward

See the full prosecution history — every USPTO and applicant action on this file, in order.

Log in to unlock

Chain of title

⤢ drag to zoom20002002200420062008201020122014201620182020Owner 1
Titlehover for detail · click to open

See the full assignment history — every owner this patent has passed through, with recordation dates and reel/frame numbers.

Log in to unlock

Term & fees

See the term timeline — pendency span, in-force span, the maintenance fees paid and both computed expiry dates.

Log in to unlock

Worldwide family

12 members · 7 offices
US1EP3JP2KR2DE2SG1TW1
this patentIP5 & PCTother officessolid = grantedhover for detail · click to open
Members
12
DOCDB simple family 27276466
Offices
7
US · EP · JP · KR
Granted
7 of 12
grant date present
Non-English titles
8
shown as filed, never translated
›IP5 & PCT — 8 members
OfficePublicationKindPublishedFiledStatusTitle
USthis patentUS-6659111-B1B19 Dec 200311 Jan 2000grantedCleaning gas and method for cleaning vacuum treatment apparatus by flowing the cleaning gas
EPEP-1020236-A2A219 Jul 200010 Jan 2000publishedReinigungsgas und Reinigungsverfahrende
EPEP-1020236-A3A326 Nov 200310 Jan 2000publishedGaz nettoyant et procédé de nettoyagefr
EPEP-1020236-B1B128 Nov 200710 Jan 2000grantedUse of cleaning gas
JPJP-2000299289-AA24 Oct 200025 Oct 1999publishedクリーニングガス及び真空処理装置のクリーニング方法ja
JPJP-3433392-B2B24 Aug 200325 Oct 1999grantedクリーニングガス及び真空処理装置のクリーニング方法ja
KRKR-20000057742-AA25 Sep 200011 Jan 2000published세정 기체 및 그를 흘려줌으로써 진공 처리 장치를세정하는 방법ko
KRKR-100363343-B1B15 Dec 200211 Jan 2000granted세정 기체 및 그를 흘려줌으로써 진공 처리 장치를세정하는 방법ko
›Other offices — 4 members
OfficePublicationKindPublishedFiledStatusTitle
DEDE-60037213-D1D110 Jan 200810 Jan 2000grantedVerwendung von Reinigungsgasde
DEDE-60037213-T2T22 Oct 200810 Jan 2000grantedVerwendung von Reinigungsgasde
SGSG-87074-A1A119 Mar 200211 Jan 2000publishedCleaning gas and method for cleaning vacuum treatment apparatus by flowing the cleaning gas
TWTW-593631-BB21 Jun 200431 Dec 1999grantedCleaning gas and method for cleaning vacuum treatment apparatus by flowing the cleaning gas

Validity challenges

See the validity challenges on record — reexaminations, IPRs and PGRs, with their institution decisions and outcomes.

Log in to unlock

Citations

See every patent this one cites and every patent that cites it back — publication, assignee, and how each one was found.

Log in to unlock